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A novel bioelectrochemical approach for chlorinated aliphatic hydrocarbons reductive and oxidative dechlorination
No full textInfluence of nitrate and sulphate reduction in the biolectrochemically assisted dechlorination of cis-DCE
No full textThis paper investigated the reductive dechlorination (RD) of cis-dichloroethylene (cis-DCE) (average influent 14.2 +/- 0.7 mu M) by a bioelectrochemical system (BES), in the presence of real contaminated groundwater containing high levels of nitrate and sulfate. The BES enhanced both the RD and competing reactions, such as nitrate and sulfate reductions, which occurred with neither an external organic carbon source nor any inoculum other than the indigenous microbial consortia in the real groundwater. In preliminary batch tests, RD and full nitrate removal occurred after a short lag phase, whereas sulfate reduction occurred slowly and alongside the RD. Under continuous flow conditions (hydraulic retention time, HRT, 1.4 d), the competition of different electron acceptors was strongly affected by the cathodic potential in the range -550 to -750 mV vs. standard hydrogen electrode (SHE). Nitrate reduction was driven to completion at all tested cathodic potentials, whereas sulfate reduction and the RD rate increased as the cathodic potential became more negative. At -750 mV vs. SHE, strong methanogenesis was also observed and became the most important sink of electrons. The overall coulombic efficiency decreased while the potential became more negative. The RD contribution was always less than 1%. Hence, greater energy consumption was required to obtain higher RD rate and better conversion. Anodic oxidation was only observed at -750 mV vs. SHE where almost 39% of residual vinyl chloride (VC) was oxidized and the sulfate was formed back from sulfide (further contributing to electric waste). (C) 2014 Elsevier Ltd. All rights reserved
Relative contribution of set cathode potential and external mass transport on TCE dechlorination in a continuous-flow bioelectrochemical reactor
No full textMicrobial bioelectrochemical systems, which use solid-state cathodes to drive the reductive degradation of contaminants such as the chlorinated hydrocarbons, are recently attracting considerable attention for bioremediation applications. So far, most of the published research has focused on analyzing the influence of key (bio)electrochemical factors influencing contaminant degradation, such as the cathode potential, whereas only few studies have examined the potential impact of mass transport phenomena on process performance. Here we analyzed the performance of a flow-through bioelectrochemical reactor, continuously fed with a synthetic groundwater containing trichloroethene at three different linear fluid velocities (from 0.3m d-1 to 1.7m d-1) and three different set cathode potentials (from -250mV to -450mV vs. the standard hydrogen electrode). The obtained results demonstrated that, in the range of fluid velocities which are characteristics for natural groundwater systems, mass transport phenomena may strongly influence the rate and extent of reductive dechlorination. Nonetheless, the relative importance of mass transport largely depends on the applied cathode potential which, in turn, controls the intrinsic kinetics of biological reactions and the underlying electron transfer mechanisms. © 2015 Elsevier Ltd
Bioelectrochemical approach for reductive and oxidative dechlorination of chlorinated aliphatic hydrocarbons (CAHs)
No full textA sequential reductive-oxidative treatment was developed in this study in a continuous-flow bioelectrochemical reactor to address bioremediation of groundwater contaminated by trichloroethene (TCE) and less-chlorinated but still harmful intermediates, such as vinyl chloride. In order to optimize the anodic compartment, whereby the oxygen-driven microbial oxidation of TCE-daughter products occurs, abiotic batch experiments were performed with various anode materials poised at +1.20 V vs. SHE (i.e., graphite rods and titanium mesh anode coated with mixed metal oxides (MMO)) and setups (i.e., electrodes embedded within a bed of silica beads or graphite granule). The MMO anode displayed higher efficiency (>90%) for oxygen generation compared to the graphite electrodes. Additionally, the graphite bed presence adversely affects oxygen generation, likely due to the oxygen scavenging. This effect was completely eliminated by replacing the graphite granules with silica beads. The anodic setups were thereafter verified in a mentioned reactor at an applied TCE loading rate of approximately 20 μM d−1 and a hydraulic retention time of 1.4 d in each compartment. The cathode consisted of a bed of graphite granules and was potentiostatically controlled at −0.65 V vs. SHE. The best reactor performance in terms of removal efficiency (i.e., >97%), removal rate (i.e., 121.8 ± 2.7 μeq L−1 d−1), and the residual concentration (i.e., 5.03 ± 0.63 μeq L−1) of chlorinated contaminants was achieved with the MMO anode placed in a silica bed. Ecotoxicity tests performed with algae confirmed these results by showing progressive toxicity reduction from inlet to cathodic and anodic effluent using this reactor configuration. © 2016 Elsevier Lt
Degradazione degli isomeri dell’esaclorocicloesano in suoli altamente contaminati mediante Ferro Zero-Valente
No full textMicrocoms study of anaerobic bioconversion of hexachlorocyclohexane in heavily contaminated soils
No full textCARD-FISH analysis of a TCE-dechlorinating biocathode operated at different set potentials
No full textBioelectrochemical systems (BES) are increasingly being considered for bioremediation applications, such as the reductive transformation of chlorinated hydrocarbons in subsurface environments. These systems typically rely on a polarized solid-state electrode (i.e. a cathode) serving as electron donor for the microbially catalyzed reductive dechlorination of chlorinated contaminants. The microorganisms involved in dechlorinating biocathodes are not still identified. Particularly, it is not clear whether the same microorganisms responsible for the reductive dechlorination in 'conventional' bioremediation systems (i.e. those based on the supply of soluble substrates as electron donors) also play a role in BES. Here, we analyzed by CARD-FISH, the microbial composition of a dechlorinating biocathode operated at different set potential, in the range from -250 mV to -750 mV (vs. the standard hydrogen electrode, SHE). The rate and extent of TCE dechlorination, as well as of competing metabolisms (i.e. methanogenesis), were found to increase as the cathode potential decreased. The higher metabolic activities observed at the more reducing cathode potentials were mirrored by a higher total biomass concentration (as DAPI-stained cells) in the cathode effluent. CARD-FISH analysis revealed that Dehalococcoides was the dominant dechlorinating bacterial genus (from 65% to 100% of Bacteria) in the range from -550 mV to -750 mV, whereas it was abruptly outcompeted by other (yet unidentified) members of the Chloroflexi phylum, when the cathode was controlled in the range from -250 mV to -450 mV. Most probably, the observed changes in the microbial composition of the biocathode were driven by changes in the dominant mechanisms of electron transfer to TCE: mediated by the electrolytic production of H-2 gas (in the range from -550 mV to -750 mV), or direct (in the range of cathode potentials from -250 mV to -450 mV)
Declorazione riduttiva del tricloroetilene in un reattore bioelettrochimico in assenza di mediazione di idrogeno
No full textRimozione degli isomeri dell’esaclorocicloesano in suoli reali altamente contaminati ad opera di un solvente ecocompatibile, acetato di etile
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